Method of storing hydrogen gas in a subsurface formation

Patent metadata

Field	Value
Publication number	US-12503639-B2
Application number	US-202318315159-A
Country	US
Kind code	B2
Filing date	May 10, 2023
Priority date	May 10, 2023
Publication date	Dec 23, 2025
Grant date	Dec 23, 2025

Abstract

A method of storing hydrogen (H 2 ) gas in a subsurface formation having an injection well, a production well and a heat well. The method includes injecting a H 2 -containing fluid stream into the subsurface formation via the injection well to form a storage composition containing a gas-phase mixture, a liquid-phase mixture and a solid matrix; and heating the subsurface formation containing the storage composition via the heat well thereby achieving a storage condition and maintaining the storage condition. The gas-phase mixture includes 10 to 90% of H 2 , 5 to 80% of methane (CH 4 ), 1 to 10% of carbon dioxide (CO 2 ), and 1 to 10% of nitrogen (N 2 ). Each % is based on a total volume of the gas-phase mixture. The liquid-phase mixture includes a water-soluble mineral; and the solid matrix includes clay, shale, slate, and minerals.

First claim

The invention claimed is:

1 . A method of storing hydrogen (H 2 ) gas in a subsurface formation having at least one injection well, at least one production well and at least one heat well penetrating the subsurface formation, comprising:
injecting a H 2 -containing fluid stream into the subsurface formation via the at least one injection well to form a storage composition containing a gas-phase mixture, a liquid-phase mixture and a solid matrix; wherein the gas-phase mixture of the storage composition comprises: 10 to 90% of H 2 ; 5 to 80% of methane (CH 4 ); 1 to 10% of carbon dioxide (CO 2 ); 1 to 10% of nitrogen (N 2 ); and each % is based on a total volume of the gas-phase mixture; wherein the liquid-phase mixture of the storage composition comprises at least one water-soluble mineral; and wherein the solid matrix of the storage composition comprises clay, shale, slate, and minerals; and heating the subsurface formation containing the storage composition via the at least one heat well thereby achieving a storage condition and maintaining the storage condition.

2 . The method of claim 1 , wherein the gas-phase mixture of the storage composition comprises:
20 to 80% of H 2 ; 10 to 70% of CH 4 ; about 5% of CO 2 ; about 5% of N 2 ; and each % is based on the total volume of the gas-phase mixture.

3 . The method of claim 1 , wherein the gas-phase mixture of the storage composition further comprises up to 5% of hydrogen sulfide (H 2 S), based on the total volume of the gas-phase mixture.

4 . The method of claim 1 , wherein the gas-phase mixture of the storage composition further comprises up to 5% of moisture (H 2 O), based on the total volume of the gas-phase mixture.

5 . The method of claim 1 , wherein the subsurface formation comprises one of a hydrocarbon-containing reservoir, a natural gas storage space, a carbon sequestration reservoir, an aquifer, a geothermal reservoir, and an in-situ leachable ore deposit.

6 . The method of claim 1 , wherein the subsurface formation comprises a rock material obtained from at least one shale selected from the group consisting of Eagle ford shale, Wolfcamp shale, Posidonia shale, Wellington shale, and Mancos shale.

7 . The method of claim 6 , wherein the rock material comprises one or more of Bentheimer sandstone, Berea sandstone, Vosges sandstone, quartz, borosilicate glass, basalt, shale, calcite, granite, dolomite, gypsum, anhydrite, mica, kaolinite, illite, montmorillonite, and coal.

8 . The method of claim 1 , wherein the at least one water-soluble mineral comprises one or more of sodium bicarbonate, sodium carbonate, sodium chloride, potassium bicarbonate, potassium carbonate, and potassium chloride.

9 . The method of claim 1 , wherein the at least one water-soluble mineral is present in the liquid-phase mixture at a concentration of 0.1 to 30 wt. % based on a total weight of the liquid-phase mixture.

10 . The method of claim 1 , wherein the at least one water-soluble mineral is sodium chloride, and wherein the sodium chloride is present in the liquid-phase mixture at a concentration of 2 to 20 wt. % based on a total weight of the liquid-phase mixture.

11 . The method of claim 1 , wherein the solid matrix of the storage composition further comprises silicate, argillite, quartz, sandstone, gypsum, conglomerate, basalt, feldspar, mica, granite, granodiorite, diorite, calcite, kaolinite, illite, montmorillonite, and sand.

12 . The method of claim 1 , wherein the storage condition has a temperature in a range of 20 to 80 degree Celsius (° C.) in the subsurface formation, a water contact angle of 15 to 60 degrees (°) under a pressure of 500 to 4000 pound-force per square inch (psi) in the subsurface formation, and a surface tension in a range of 40 to 85 dynes per centimeter (dynes/cm) under the pressure of 500 to 4000 psi in the subsurface formation.

13 . The method of claim 1 , wherein the storage condition has a pressure of 300 to 5000 psi in the subsurface formation, a water contact angle with the subsurface formation in a range of 10 to 50° under a temperature of 30 to 70° C. in the subsurface formation, and a surface tension in a range of 50 to 80 dynes/cm under the temperature of 30 to 70° C. in the subsurface formation.

14 . The method of claim 1 , wherein the gas-phase mixture of the storage composition comprises about 60% of H 2 , about 40% of CH 4 , about 5% of CO 2 , about 5% of N 2 , and each % is based on the total volume of the gas-phase mixture;
the liquid-phase mixture comprises 2 to 5 wt. % of NaCl based on a total weight of the liquid-phase mixture; and the storage condition has a temperature in a range of 30 to 40° C.

15 . The method of claim 1 , further comprising:
withdrawing the gas-phase mixture of the storage composition from the subsurface formation via the at least one production well; introducing the gas-phase mixture into a hydrogen purification device comprising a plurality of hydrogen-selective membranes; wherein the plurality of hydrogen-selective membranes are permeable to hydrogen gas, but are at least substantially impermeable to other components in the gas-phase mixture; passing the gas-phase mixture through the plurality of hydrogen-selective membranes in the hydrogen purification device thereby allowing hydrogen gas to pass through the hydrogen-selective membrane and rejecting other components in the gas-phase mixture to form a residue composition; and collecting the hydrogen gas after passing and recycling the residue composition.

16 . The method of claim 15 , wherein the plurality of hydrogen-selective membranes in the hydrogen purification device is arranged in parallel, and wherein each membrane of the plurality of hydrogen-selective membranes is placed in a plane perpendicular to the direction of the gas-phase mixture flow in the hydrogen purification device.

17 . The method of claim 1 , wherein the at least one heat well is in the form of a closed-loop pipeline having an aboveground loop part and an underground loop part.

18 . The method of claim 17 , wherein the underground loop part has a helix shape.

19 . The method of claim 17 , wherein the underground loop part includes a perforated casing.

Assignees

• Univ King Fahd Pet & Minerals

Inventors

• Haq Md Bashirul
• Al Shehri Dhafer Abdullah
• Muhammed Nasiru Salahu

Classifications

• B65G5/005

  in porous layers · CPC title

• B01D53/226 Primary

  in serial connexion · CPC title

• C09K8/594 Primary

  Compositions used in combination with injected gas {, e.g. CO2 orcarbonated gas}(C09K8/592 takes precedence) · CPC title